Parametric sensitivity analysis of direct contact membrane distillation

被引:27
作者
Abu Al-Rub, FA
Banat, F
Beni-Melhim, K
机构
[1] United Arab Emirates Univ, Dept Chem & Petr Engn, Al Ain, U Arab Emirates
[2] Univ Bahrain, Dept Chem Engn, Al Manamah, Bahrain
[3] Potash Arab Co, Kerak, Jordan
关键词
membrane distillation; sensitivity; direct contact; flux;
D O I
10.1081/SS-120006160
中图分类号
O6 [化学];
学科分类号
0703 ;
摘要
Membrane distillation is a thermally driven mass transfer in which a porous hydrophobic membrane separates two liquid phases and a temperature difference is maintained as the driving force. In this study, the technique of direct contact membrane distillation (DCMD) process, where the liquid phases are in direct contact with both sides of the membrane, has been investigated for the case of pure water production. Parametric sensitivity analysis and temperature polarization factor are used to study the sensitivity of the mass flux to the different parameters associated with DCMD for water production, and the effect of these parameters on the thermal efficiency of the DCMD process has been investigated. The results obtained show that the mass flux of pure water production is highly sensitive to the feed bulk temperature, and at low flow rates of hot and cold fluids, to the heat transfer coefficients. Results also show that increasing membrane thickness decreases the mass flux of pure water and decreases temperature polarization effect. In addition, results show that temperature polarization effect becomes significant as feed bulk temperature increases.
引用
收藏
页码:3245 / 3271
页数:27
相关论文
共 18 条
  • [1] Abu Al-Rub F, 1999, SEPAR SCI TECHNOL, V34, P2817
  • [2] [Anonymous], [No title captured]
  • [3] On the effect of inert gases in breaking the formic acid-water azeotrope by gas-gap membrane distillation
    Banat, FA
    Abu Al-Rub, F
    Jumah, R
    Shannag, M
    [J]. CHEMICAL ENGINEERING JOURNAL, 1999, 73 (01) : 37 - 42
  • [4] Application of Stefan-Maxwell approach to azeotropic separation by membrane distillation
    Banat, FA
    Abu Al-Rub, F
    Jumah, R
    Al-Shannag, M
    [J]. CHEMICAL ENGINEERING JOURNAL, 1999, 73 (01) : 71 - 75
  • [5] Theoretical investigation of membrane distillation role in breaking the formic acid-water azeotropic point: Comparison between Fickian and Stefan-Maxwell-based models
    Banat, FA
    Abu Al-Rub, F
    Jumah, R
    Shannag, M
    [J]. INTERNATIONAL COMMUNICATIONS IN HEAT AND MASS TRANSFER, 1999, 26 (06) : 879 - 888
  • [6] Simultaneous removal of acetone and ethanol from aqueous solutions by membrane distillation: prediction using the Fick's and the exact and approximate Stefan-Maxwell relations
    Banat, FA
    Al-Rub, FA
    Shannag, M
    [J]. HEAT AND MASS TRANSFER, 1999, 35 (05) : 423 - 431
  • [7] BANAT FA, 2001, MEMBRANE DISTILLATIO
  • [8] ROLE OF HEAT AND MASS-TRANSFER IN MEMBRANE DISTILLATION PROCESS
    BANDINI, S
    GOSTOLI, C
    SARTI, GC
    [J]. DESALINATION, 1991, 81 (1-3) : 91 - 106
  • [9] Bird R.B., 2006, TRANSPORT PHENOMENA, Vsecond, DOI 10.1002/aic.690070245
  • [10] CHENG DY, 1989, Patent No. 4316772